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Article: Comparison of startup performance of four anaerobic reactors for the treatment of high-strength wastewater

TitleComparison of startup performance of four anaerobic reactors for the treatment of high-strength wastewater
Authors
Issue Date1994
PublisherElsevier BV. The Journal's web site is located at http://www.elsevier.com/locate/resconrec
Citation
Resources, Conservation And Recycling, 1994, v. 11 n. 1-4, p. 123-138 How to Cite?
AbstractAn experimental study was carried out to compare the startup performance of four equal-volume anaerobic reactors of different design operated in parallel at 37°C. The four reactors, namely, (a) upflow anaerobic sludge blanket (UASB), (b) hybrid of UASB and anaerobic filter, (c) fluidized bed and (d) expanded bed, were seeded with sludge from the anaerobic digester of a local municipal wastewater treatment plant and tested with synthetic wastewater comprising milk and sucrose with balanced nutrients and trace metals. The volumetric COD loading was increased gradually from the initial 0.5-1 g L-1 d-1 to 20 g L-1 d-1 after 70 days. During this startup period, the COD levels in wastewater were gradually increased from the initial 500-1000 mg L-1 to 6500 mg L-1, whereas the hydraulic retention time (HRT) was reduced from 24-48 h to 8 h. After the acclimation, the four reactors were tested at the loading rate of about 20 g L-1 d-1, but at three different levels of COD (6000, 4000, 2600 mg L-1) and HRT (8, 5.7, 3 h). The percentage of COD removal from wastewater in an anaerobic reactor appeared to be mainly dependent on the volumetric COD loading rate, and relatively insensitive to the COD level in wastewater and the HRT. At the COD loading rate of about 20 g L-1 d-1, COD reduction was about 95% for the UASB and the hybrid reactors, but was about 80% for the fluidized bed and expanded bed reactors.
Persistent Identifierhttp://hdl.handle.net/10722/150029
ISSN
2023 Impact Factor: 11.2
2023 SCImago Journal Rankings: 2.770
ISI Accession Number ID

 

DC FieldValueLanguage
dc.contributor.authorFang, HHPen_US
dc.contributor.authorChui, HKen_US
dc.date.accessioned2012-06-26T06:01:10Z-
dc.date.available2012-06-26T06:01:10Z-
dc.date.issued1994en_US
dc.identifier.citationResources, Conservation And Recycling, 1994, v. 11 n. 1-4, p. 123-138en_US
dc.identifier.issn0921-3449en_US
dc.identifier.urihttp://hdl.handle.net/10722/150029-
dc.description.abstractAn experimental study was carried out to compare the startup performance of four equal-volume anaerobic reactors of different design operated in parallel at 37°C. The four reactors, namely, (a) upflow anaerobic sludge blanket (UASB), (b) hybrid of UASB and anaerobic filter, (c) fluidized bed and (d) expanded bed, were seeded with sludge from the anaerobic digester of a local municipal wastewater treatment plant and tested with synthetic wastewater comprising milk and sucrose with balanced nutrients and trace metals. The volumetric COD loading was increased gradually from the initial 0.5-1 g L-1 d-1 to 20 g L-1 d-1 after 70 days. During this startup period, the COD levels in wastewater were gradually increased from the initial 500-1000 mg L-1 to 6500 mg L-1, whereas the hydraulic retention time (HRT) was reduced from 24-48 h to 8 h. After the acclimation, the four reactors were tested at the loading rate of about 20 g L-1 d-1, but at three different levels of COD (6000, 4000, 2600 mg L-1) and HRT (8, 5.7, 3 h). The percentage of COD removal from wastewater in an anaerobic reactor appeared to be mainly dependent on the volumetric COD loading rate, and relatively insensitive to the COD level in wastewater and the HRT. At the COD loading rate of about 20 g L-1 d-1, COD reduction was about 95% for the UASB and the hybrid reactors, but was about 80% for the fluidized bed and expanded bed reactors.en_US
dc.languageengen_US
dc.publisherElsevier BV. The Journal's web site is located at http://www.elsevier.com/locate/resconrecen_US
dc.relation.ispartofResources, Conservation and Recyclingen_US
dc.titleComparison of startup performance of four anaerobic reactors for the treatment of high-strength wastewateren_US
dc.typeArticleen_US
dc.identifier.emailFang, HHP:hrechef@hkucc.hku.hken_US
dc.identifier.authorityFang, HHP=rp00115en_US
dc.description.naturelink_to_subscribed_fulltexten_US
dc.identifier.doi10.1016/0921-3449(94)90084-1en_US
dc.identifier.scopuseid_2-s2.0-0028457163en_US
dc.identifier.volume11en_US
dc.identifier.issue1-4en_US
dc.identifier.spage123en_US
dc.identifier.epage138en_US
dc.identifier.isiWOS:A1994NY74000012-
dc.publisher.placeNetherlandsen_US
dc.identifier.scopusauthoridFang, HHP=7402542625en_US
dc.identifier.scopusauthoridChui, HK=7006642070en_US
dc.identifier.issnl0921-3449-

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